JPH0665585A - Apparatus for dechlorination and waste gas conversion for waste plastic - Google Patents
Apparatus for dechlorination and waste gas conversion for waste plasticInfo
- Publication number
- JPH0665585A JPH0665585A JP4220433A JP22043392A JPH0665585A JP H0665585 A JPH0665585 A JP H0665585A JP 4220433 A JP4220433 A JP 4220433A JP 22043392 A JP22043392 A JP 22043392A JP H0665585 A JPH0665585 A JP H0665585A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- dechlorination
- waste plastic
- water
- water gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 229920003023 plastic Polymers 0.000 title claims abstract description 41
- 239000004033 plastic Substances 0.000 title claims abstract description 41
- 239000002699 waste material Substances 0.000 title claims abstract description 35
- 238000006298 dechlorination reaction Methods 0.000 title claims abstract description 25
- 238000006243 chemical reaction Methods 0.000 title abstract description 9
- 239000002912 waste gas Substances 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 53
- 239000003054 catalyst Substances 0.000 claims abstract description 27
- 229920000915 polyvinyl chloride Polymers 0.000 claims abstract description 11
- 239000004800 polyvinyl chloride Substances 0.000 claims abstract description 11
- 230000000382 dechlorinating effect Effects 0.000 claims abstract 2
- 238000002309 gasification Methods 0.000 claims description 30
- 238000002844 melting Methods 0.000 claims description 2
- 230000008018 melting Effects 0.000 claims description 2
- 239000000446 fuel Substances 0.000 abstract description 9
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 abstract description 4
- 239000000203 mixture Substances 0.000 abstract description 3
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 abstract description 2
- 229910000423 chromium oxide Inorganic materials 0.000 abstract description 2
- 229910000476 molybdenum oxide Inorganic materials 0.000 abstract description 2
- 229910000480 nickel oxide Inorganic materials 0.000 abstract description 2
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical compound [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 abstract description 2
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 abstract description 2
- 238000003763 carbonization Methods 0.000 abstract 3
- 239000007789 gas Substances 0.000 description 25
- 238000010438 heat treatment Methods 0.000 description 11
- 238000011084 recovery Methods 0.000 description 8
- 239000010812 mixed waste Substances 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 239000004449 solid propellant Substances 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 2
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000005539 carbonized material Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、都市ごみや産業廃棄物
として廃棄される廃プラスチックの処理装置に関し、よ
り詳細には、混合廃プラスチックの溶融工程において脱
塩素を行った後、廃プラスチックの熱分解および触媒存
在下での炭化物の水性ガス化反応を行ってガス燃料を製
造する廃プラスチックの脱塩素・水性ガス化装置に関す
るものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for treating waste plastics discarded as municipal wastes or industrial wastes. More specifically, the present invention relates to an apparatus for treating waste plastics after dechlorination in a melting process of mixed waste plastics. The present invention relates to a dechlorination / water gasification device for waste plastics, which produces a gas fuel by carrying out a water gasification reaction of a carbide in the presence of a catalyst by thermal decomposition.
【0002】[0002]
【従来の技術】近年、混合廃プラスチックの処理方法と
して、資源有効利用の面から、廃プラスチックの燃料化
(固形燃料(RDF)、油化、ガス化)が見直されてい
る。しかし、混合廃プラスチックに含まれるポリ塩化ビ
ニルの塩素分が油化工程や固形燃料使用時に塩化水素化
して装置腐食などの障害を招く上に、得られた固形燃料
に塩素分の増加をもたらす難点があるため、現在ではポ
リ塩化ビニルを含有しない廃プラスチックの燃料化が行
われている。2. Description of the Related Art Recently, as a method for treating mixed waste plastics, the use of waste plastics as fuel (solid fuel (RDF), oilification, gasification) has been reconsidered from the viewpoint of effective use of resources. However, the chlorine content of polyvinyl chloride contained in the mixed waste plastics causes hydrogen chloride during the oilification process and the use of solid fuel, which causes equipment corrosion and other problems, and the chlorine content of the obtained solid fuel increases. Therefore, waste plastics that do not contain polyvinyl chloride are currently being used as fuel.
【0003】廃プラスチックの代表的な加熱分解方法と
しては、流動床式、スクリュー式、触媒を用いる接触式
がある。Typical thermal decomposition methods for waste plastics include a fluidized bed type, a screw type, and a catalytic type using a catalyst.
【0004】他方、水素の製造は、古くはコークスの水
性ガス化反応、最近では天然ガス・ナフサあるいは重質
油の部分酸化反応などによって行われている。On the other hand, the production of hydrogen is carried out by water gasification reaction of coke in the old days, and recently by partial oxidation reaction of natural gas / naphtha or heavy oil.
【0005】[0005]
【発明が解決しようとする課題】廃プラスチック中にポ
リ塩化ビニルが含まれていると、廃プラスチックの溶融
時にポリ塩化ビニルの脱塩素による激しいコーキングが
起きる。このコーキング成分である炭化物をいかにして
連続的に取り出し、効率よく水性ガス化するかが、廃プ
ラスチックのガス燃料化を実用化する上での重要な課題
である。When polyvinyl chloride is contained in the waste plastic, violent caulking occurs due to dechlorination of the polyvinyl chloride during melting of the waste plastic. How to continuously take out the carbide, which is the caulking component, and efficiently convert it into water gas is an important issue for practical use of waste plastics as a gas fuel.
【0006】本発明は、上記の実情に鑑みてなされたも
のであって、その目的は、混合廃プラスチック中のポリ
塩化ビニルの脱塩素を行った後、生成したコーキング成
分(炭化物)を水性ガス化反応によってガス燃料化する
ことができる装置を提供することにある。The present invention has been made in view of the above circumstances, and an object of the present invention is to dechlorinate polyvinyl chloride contained in a mixed waste plastic, and then to remove the caulking component (carbide) produced as a water gas. An object of the present invention is to provide a device that can be converted into gas fuel by a chemical reaction.
【0007】[0007]
【課題を解決するための手段】本発明は、上記課題を解
決すべく工夫されたもので、廃プラスチック溶融時に球
状で比較的大きな孔径を有するポラスな水性ガス化触媒
を廃プラスチックに混在させておき、触媒の多孔中に入
った溶融プラスチックをコンキングさせ、生じた炭化物
が付着した触媒を傾斜移動させながら効率よく炭化物を
水性ガス化するようにした廃プラスチックの脱塩素・水
性ガス化装置である。The present invention has been devised in order to solve the above-mentioned problems. When a waste plastic is melted, a porous water gasification catalyst having a spherical shape and a relatively large pore size is mixed with the waste plastic. The dechlorination and water gasification equipment for waste plastics, in which the molten plastic that has entered the pores of the catalyst is conquered, and the carbonized material is efficiently gasified into water while slanting the catalyst to which the resulting carbide is attached. .
【0008】すなわち、本発明による廃プラスチックの
脱塩素・水性ガス化装置は、球状の水性ガス化触媒と共
に供給されたポリ塩化ビニル含有廃プラスチックを溶融
・脱塩素し、生じた炭化物を触媒上に付着させる脱塩素
ゾーンと、触媒上の炭化物を水蒸気と反応させて水性ガ
スを生成する水性ガス化ゾーンとを備えたものである。That is, the waste plastic dechlorination / water gasification apparatus according to the present invention melts and dechlorines the polyvinyl chloride-containing waste plastic supplied together with the spherical water gasification catalyst and deposits the resulting carbide on the catalyst. It is provided with a dechlorination zone for deposition and a water gasification zone for reacting the carbide on the catalyst with water vapor to produce water gas.
【0009】上記脱塩素ゾーンとしては、好ましくは脱
塩素スクリューフィーダが用いられ、上記水性ガス化ゾ
ーンとしては、好ましくは傾斜状の水性ガス化スクリュ
ーフィーダが用いられる。A dechlorination screw feeder is preferably used as the dechlorination zone, and an inclined water gasification screw feeder is preferably used as the water gasification zone.
【0010】水性ガス化触媒としては、酸化ニッケル、
酸化モリブデン、酸化鉄、酸化クロムなどからなるポラ
スな球状物が使用される。As the water gasification catalyst, nickel oxide,
Porous spherical particles made of molybdenum oxide, iron oxide, chromium oxide, etc. are used.
【0011】[0011]
【実施例】本発明による廃プラスチックの脱塩素・水性
ガス化装置の一例を図1に示す。バーナ(1a)を備えた加
熱炉(1) の上方に、攪拌機(16)を備えた廃プラスチック
タンク(2) が配置され、脱塩素スクリューフィーダ(3)
が加熱炉(1) の頂部に水平に内装され、水性ガス化スク
リューフィーダ(5) が加熱炉(1) の底部に傾斜状に内装
されている。そして、廃プラスチックタンク(2) の底部
が落下路(4) を介して脱塩素スクリューフィーダ(3) の
始端部に連絡され、同スクリューフィーダ(3) の終端部
が垂直スクリューフィーダ(6) によって水性ガス化スク
リューフィーダ(5) の始端部に連絡されている。水性ガ
ス化スクリューフィーダ(5) の終端部から廃プラスチッ
クタンク(2) へ球状触媒(C) を戻す触媒回送管(8) が配
されている。加熱炉(1) の中央部には、ボイラー(7) の
蛇行管(7a)が配され、ボイラー(7) から水性ガス化スク
リューフィーダ(5) の終端部付近に水蒸気供給管(9)が
配されている。脱塩素スクリューフィーダ(3) の中間部
および加熱炉(1) の頂部からガス洗浄塔(10)へ排ガス管
(11)(12)がそれぞれ配され、また水性ガス化スクリュー
フィーダ(5) の始端部付近から水性ガス回収装置(15)へ
水性ガス回収管(13)が配され、同回収装置(15)から加熱
炉(1) のバーナ(1a)へ水性ガス供給管(14)が配されてい
る。EXAMPLE FIG. 1 shows an example of a dechlorination / water gasification apparatus for waste plastic according to the present invention. A waste plastic tank (2) equipped with a stirrer (16) is arranged above the heating furnace (1) equipped with a burner (1a), and a dechlorination screw feeder (3) is installed.
Is horizontally installed on the top of the heating furnace (1), and the water gasification screw feeder (5) is installed on the bottom of the heating furnace (1) in an inclined shape. Then, the bottom of the waste plastic tank (2) is connected to the beginning of the dechlorination screw feeder (3) via the drop path (4), and the end of the screw feeder (3) is connected by the vertical screw feeder (6). It is connected to the beginning of the water gasification screw feeder (5). A catalyst feed pipe (8) for returning the spherical catalyst (C) from the end of the water gasification screw feeder (5) to the waste plastic tank (2) is arranged. In the center of the heating furnace (1), a meandering pipe (7a) of the boiler (7) is arranged, and a steam supply pipe (9) is installed from the boiler (7) near the end of the water gasification screw feeder (5). It is distributed. Exhaust gas pipe from the middle part of the dechlorination screw feeder (3) and the top of the heating furnace (1) to the gas cleaning tower (10)
(11) (12) are respectively arranged, and the water gas recovery pipe (13) is arranged from the vicinity of the starting end of the water gasification screw feeder (5) to the water gas recovery device (15), and the recovery device (15) To the burner (1a) of the heating furnace (1) is provided a water gas supply pipe (14).
【0012】上記構成の脱塩素・水性ガス化装置におい
て、ポリ塩化ビニルを含む廃プラスチックと水性ガス化
用の球状触媒(C) とは廃プラスチックタンク(2) に投入
され、ここで攪拌機(16)により混合される。廃プラスチ
ックと球状触媒の混合物はついで廃プラスチックタンク
(2) から落下路(4) を経て脱塩素スクリューフィーダ
(3) の始端部へ落下する。廃プラスチックは、ここで同
フィーダ(3) で終端部へ送られる間に加熱炉(1) の熱に
よって350〜400℃程度に加熱され、溶融されると
共に脱塩素される。廃プラスチックの脱塩素により生じ
た塩化水素ガスは排ガス管(11)を経てガス洗浄塔(10)に
送られてここで洗浄され、塩酸として回収される。微量
の炭化水素もその回収装置によって回収される。In the dechlorination / water gasification apparatus having the above-mentioned structure, the waste plastic containing polyvinyl chloride and the spherical catalyst (C) for water gasification are put into the waste plastic tank (2), where the stirrer (16 ) Is mixed. The mixture of waste plastic and spherical catalyst is followed by the waste plastic tank
Dechlorination screw feeder from (2) via drop path (4)
It falls to the beginning of (3). The waste plastic is heated to about 350 to 400 ° C. by the heat of the heating furnace (1) while being sent to the end portion by the feeder (3), melted and dechlorinated. Hydrogen chloride gas generated by dechlorination of waste plastic is sent to the gas cleaning tower (10) via the exhaust gas pipe (11), where it is cleaned and recovered as hydrochloric acid. A minute amount of hydrocarbons is also recovered by the recovery device.
【0013】脱塩素された溶融プラスチックはコーキン
グさせられ、生じた炭化物は比較的大きな孔径を有する
ポラスな水性ガス化球状触媒(C) の表面に付着する。炭
化物を付着した球状触媒は脱塩素スクリューフィーダ
(3) の終端部から垂直スクリューフィーダ(6) を経て傾
斜状の水性ガス化スクリューフィーダ(5) の始端部へ送
られる。そして球状触媒は同フィーダ(5) を終端部へ移
動しながら、加熱炉(1)の燃焼熱によって700℃程度
に加熱される。また、加熱炉(1) の熱によって生成され
た水蒸気がボイラー(7) から水蒸気供給管(9) を経て水
性ガス化スクリューフィーダ(5) の終端部付近に供給さ
れる。その結果、球状触媒上の炭化物と水蒸気が反応し
て、水性ガスが生成する。こうして生じた水性ガスは、
水性ガス回収管(13)を経て水性ガス回収装置(15)へ送ら
れ、その一部は加熱炉(1) のバーナ(1a)へ燃料として供
給され、残部は他の用途に利用される。水性ガス化スク
リューフィーダ(5) の終端部から出た球状触媒(C) は再
び廃プラスチックタンク(2)へ戻される。The dechlorinated molten plastic is coked, and the resulting carbide is deposited on the surface of a porous water gasification spherical catalyst (C) having a relatively large pore size. Spherical catalyst with carbide attached is a dechlorination screw feeder
It is fed from the terminal end of (3) through a vertical screw feeder (6) to the starting end of an inclined water gasification screw feeder (5). Then, the spherical catalyst is heated to about 700 ° C. by the combustion heat of the heating furnace (1) while moving the feeder (5) to the end portion. Further, the steam generated by the heat of the heating furnace (1) is supplied from the boiler (7) through the steam supply pipe (9) to the vicinity of the end of the water gasification screw feeder (5). As a result, the carbide on the spherical catalyst reacts with water vapor to generate water gas. The water gas thus generated is
It is sent to the water gas recovery device (15) through the water gas recovery pipe (13), a part of it is supplied to the burner (1a) of the heating furnace (1) as fuel, and the rest is used for other purposes. The spherical catalyst (C) discharged from the end of the water gasification screw feeder (5) is returned to the waste plastic tank (2) again.
【0014】[0014]
【発明の効果】本発明による廃プラスチックの脱塩素・
水性ガス化装置は以上の通り構成されているので、混合
廃プラスチック中のポリ塩化ビニルの脱塩素を溶融熱分
解により行い、生成したコーキング成分(炭化物)を水
性ガス化反応によってガス燃料化することができる。こ
うして、廃プラスチックのガス燃料化を実用化すること
ができる。EFFECT OF THE INVENTION Dechlorination of waste plastic according to the present invention
Since the water gasifier is configured as described above, dechlorination of polyvinyl chloride in mixed waste plastics is carried out by melt pyrolysis, and the generated coking component (carbide) is converted to gas fuel by water gasification reaction. You can In this way, it is possible to put the waste plastic into a gas fuel for practical use.
【図1】廃プラスチックの脱塩素・水性ガス化装置を示
す垂直断面図である。FIG. 1 is a vertical sectional view showing a dechlorination / water gasification device for waste plastic.
(1) …加熱炉 (2) …廃プラスチックタンク (3) …脱塩素スクリューフィーダ (4) …落下路 (5) …水性ガス化スクリューフィーダ (6) …垂直スクリューフィーダ (7) …ボイラー (8) …触媒回送管 (9) …水蒸気供給管 (10)…ガス洗浄塔 (11)(12)…排ガス管 (13)…水性ガス回収管 (14)…水性ガス供給管 (15)…水性ガス回収装置 (1)… Heating furnace (2)… Waste plastic tank (3)… Dechlorination screw feeder (4)… Drop path (5)… Water gasification screw feeder (6)… Vertical screw feeder (7)… Boiler (8 )… Catalyst transfer pipe (9)… Steam supply pipe (10)… Gas cleaning tower (11) (12)… Exhaust gas pipe (13)… Water gas recovery pipe (14)… Water gas supply pipe (15)… Water gas Recovery device
フロントページの続き (72)発明者 濱 利雄 大阪市此花区西九条5丁目3番28号 日立 造船株式会社内 (72)発明者 平田 直子 大阪市此花区西九条5丁目3番28号 日立 造船株式会社内Front page continuation (72) Inventor Toshio Hama 5-3-28 Nishikujo, Konohana-ku, Osaka City Hitachi Shipbuilding Co., Ltd. In the company
Claims (1)
ポリ塩化ビニル含有廃プラスチックを溶融・脱塩素化
し、生じた炭化物を触媒上に付着させる脱塩素ゾーン
と、触媒上の炭化物を水蒸気と反応させて水性ガスを生
成する水性ガス化ゾーンとを備えた、廃プラスチックの
脱塩素・水性ガス化装置。1. A dechlorination zone for melting and dechlorinating polyvinyl chloride-containing waste plastic supplied together with a spherical water gasification catalyst, and adhering the resulting carbide onto the catalyst, and reacting the carbide on the catalyst with steam. A dechlorination / water gasification device for waste plastic, which is provided with a water gasification zone for generating water gas.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4220433A JPH0665585A (en) | 1992-08-19 | 1992-08-19 | Apparatus for dechlorination and waste gas conversion for waste plastic |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4220433A JPH0665585A (en) | 1992-08-19 | 1992-08-19 | Apparatus for dechlorination and waste gas conversion for waste plastic |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0665585A true JPH0665585A (en) | 1994-03-08 |
Family
ID=16751037
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4220433A Withdrawn JPH0665585A (en) | 1992-08-19 | 1992-08-19 | Apparatus for dechlorination and waste gas conversion for waste plastic |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0665585A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995015244A1 (en) * | 1993-11-26 | 1995-06-08 | Reinhard Fischer | Process and apparatus for recycling waste polymers |
EP0699735A1 (en) * | 1994-08-31 | 1996-03-06 | LINDE-KCA-Dresden GmbH | Process for combined working up of PVC and other chlorinated hydrocarbons |
KR100435218B1 (en) * | 2001-03-24 | 2004-06-09 | 구재완 | manufacturing apparatus for solid fuel using combustible waste |
JP2006265356A (en) * | 2005-03-23 | 2006-10-05 | Honda Motor Co Ltd | Apparatus for treating plastic-containing waste and treatment method |
-
1992
- 1992-08-19 JP JP4220433A patent/JPH0665585A/en not_active Withdrawn
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995015244A1 (en) * | 1993-11-26 | 1995-06-08 | Reinhard Fischer | Process and apparatus for recycling waste polymers |
EP0699735A1 (en) * | 1994-08-31 | 1996-03-06 | LINDE-KCA-Dresden GmbH | Process for combined working up of PVC and other chlorinated hydrocarbons |
KR100435218B1 (en) * | 2001-03-24 | 2004-06-09 | 구재완 | manufacturing apparatus for solid fuel using combustible waste |
JP2006265356A (en) * | 2005-03-23 | 2006-10-05 | Honda Motor Co Ltd | Apparatus for treating plastic-containing waste and treatment method |
JP4520888B2 (en) * | 2005-03-23 | 2010-08-11 | 本田技研工業株式会社 | Waste plastic processing equipment and processing method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20240240093A1 (en) | Two-stage plasma process for converting waste into fuel gas and apparatus therefor | |
US6333015B1 (en) | Synthesis gas production and power generation with zero emissions | |
US4950309A (en) | Process for the conversion of toxic organic substances to useful products | |
US4397656A (en) | Process for the combined coking and gasification of coal | |
EP0423401B1 (en) | Two-stage coal gasification process | |
CN101445750B (en) | Method for catalyzing and gasifying carbon-based compounds by using alkali molten salt and device thereof | |
US6638396B1 (en) | Method and apparatus for processing a waste product | |
JP6226423B2 (en) | Production of synthesis gas from oxidized biomass by heating with hot gas obtained by oxidation of residual product | |
JPS62501053A (en) | Decomposition of toxic compounds | |
JPS6140279B2 (en) | ||
JPS5844601B2 (en) | Bubunsanganiyorgouseigasno seizouhouhou | |
JPS61101232A (en) | Method and plant for cleaning waste gas | |
CN211394370U (en) | System for pyrolysis of junked tire of boiler flue gas of thermal power plant | |
US3710737A (en) | Method for producing heat | |
EP0512305B1 (en) | Method to convert refuse derived fuel into a combustible gas | |
JPH0665585A (en) | Apparatus for dechlorination and waste gas conversion for waste plastic | |
JP3506893B2 (en) | Method for producing carbide from waste solid fuel | |
JPH11199215A (en) | Production of activated carbon from refuse-derived fuel | |
Sergeev et al. | Gasification and plasma gasification as type of the thermal waste utilization | |
JP2005154516A (en) | Apparatus for chemical recycling of waste plastic | |
JPS61106696A (en) | Gasifier for coal, wood or the like | |
JPH09504822A (en) | Method for reducing hydrogen halide content in synthesis gas | |
JP3696992B2 (en) | Heat treatment method for waste | |
JPH11106211A (en) | Production of active carbon from refuse derived fuel | |
KR20010067332A (en) | Process and plant for processing liquid and/or solid organic waste substances |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Application deemed to be withdrawn because no request for examination was validly filed |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 19991102 |